US2352059A - Treatment of hydrocarbons - Google Patents

Treatment of hydrocarbons Download PDF

Info

Publication number
US2352059A
US2352059A US330613A US33061340A US2352059A US 2352059 A US2352059 A US 2352059A US 330613 A US330613 A US 330613A US 33061340 A US33061340 A US 33061340A US 2352059 A US2352059 A US 2352059A
Authority
US
United States
Prior art keywords
treatment
hydrocarbons
sulphuretted
sulphur
molecules
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US330613A
Inventor
Woog Paul
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Application granted granted Critical
Publication of US2352059A publication Critical patent/US2352059A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G35/00Reforming naphtha
    • C10G35/04Catalytic reforming
    • C10G35/06Catalytic reforming characterised by the catalyst used

Definitions

  • the object of the present invention is an improvement in the treatment of hydrocarbons in order to increase their anti-knock properties, by subjecting them to a catalytic desulfurizing and reforming in the presence of sulphur derivatives.
  • the reaction on which the process is based is the transformation of organic combinations of sulphur by heat, in the zone of 300 to 500 C., in the presence of suitable catalysts and in contact with the fuel to be treated.
  • the catalyst used may be cadmium, molybdenum, tungsten sulphide, natural or activated clayey earths, alumina, magnesia, quick-lime, silica gel, pumice-stone, kieselguhr, active charcoal, alkaline-earth silicates or mixtures of these substances.
  • the sulphuretted molecules required for the foregoing reactions may be'molecules that exist naturally in the products to be treated; use may also be made of artificially prepared sulphuretted molecules or of molecules that exist naturally in some sulphuretted products other than liquid hydrocarbon fuels (oils of sulphurized schists, residues of washing or refining processes, suitable fractions of sulphurized petroleums, etc.) Motor fuels which are naturally sulphurized may there fore be enriched in organic sulphur in order to make them capable of being subjected to a more eflicient treatment; on the other hand, unsuiphurized motor fuels may also be treated after the addition of suitable quantities of sulphuretted products.
  • reaction may be written:
  • the treatment for carrying out the present process may be effected in the vapor phase or in the liquid phase, at atmospheric pressure or under pressure.
  • Example I The product to be treated may be obtained for example from a crude Irak petroleum which is rich in sulphuretted organic combinations or, on the contrary, from a crude Texas petroleum to which 5 to 6% of sulphurized schist oils have beenadded.
  • the product which has been completely vaporized in a' suitable still, is introduced at atmospheric pressure into a chamber filled with catalyst.
  • This catalyst is raised to a temperature between 350 and 450 C. but which is so regulated as to obtain the best reaction while producing the minimum quantity of gas. With a suitable adjustment, said gas can be limited to the sulphuretted hydrogen produced by the reaction and the losses are therefore reduced to a minimum.
  • Example II The motor fuel to be treated, which has previously been enriched in sulphuretted organic combinations, is heated in a closed vessel; the pressure which is set up in the vessel is obviously proportional to the temperature obtained. Th operation may be discontinuous or continuous, the product circulating in the latter case under the eflect of suitably arranged pumps. In any case, the product which has been raised to the reaction temperature is placed in the presence of similar catalysts to those referred to above.
  • the products obtained by means of the treatment which is the object of the present invention contain practically no sulphur. They show considerably improved anti-knock properties and a very satisfactory susceptibility to tetraethyl lead.
  • I claimr A process of producing motor fuels of high antlknock value by a desulfurizing and reforming action, which comprises completely vaporizing a light hydrocarbon oil containing from about 5 to 6 per cent of an added sulfurized schist oil, passing said vapors in contact with a reforming catalyst at a temperature within the range of about 300 to 500 C. and recovering a desulfurized and reformed motor fuel of .high anti-knock value.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Description

Patented June 20, 1944 TREATMENT OF HYDROCARBONS Paul Woog, Paris, France; vested in; the Alien Property Custodian No Drawing. Application April 19, 1940, Serial No. 330,613. In France May 6, 1939 1 Claim.
The object of the present invention is an improvement in the treatment of hydrocarbons in order to increase their anti-knock properties, by subjecting them to a catalytic desulfurizing and reforming in the presence of sulphur derivatives.
The reaction on which the process is based is the transformation of organic combinations of sulphur by heat, in the zone of 300 to 500 C., in the presence of suitable catalysts and in contact with the fuel to be treated.
The catalyst used may be cadmium, molybdenum, tungsten sulphide, natural or activated clayey earths, alumina, magnesia, quick-lime, silica gel, pumice-stone, kieselguhr, active charcoal, alkaline-earth silicates or mixtures of these substances.
The sulphuretted molecules required for the foregoing reactions (neutral sulphides, mercaptans, etc. etc.) may be'molecules that exist naturally in the products to be treated; use may also be made of artificially prepared sulphuretted molecules or of molecules that exist naturally in some sulphuretted products other than liquid hydrocarbon fuels (oils of sulphurized schists, residues of washing or refining processes, suitable fractions of sulphurized petroleums, etc.) Motor fuels which are naturally sulphurized may there fore be enriched in organic sulphur in order to make them capable of being subjected to a more eflicient treatment; on the other hand, unsuiphurized motor fuels may also be treated after the addition of suitable quantities of sulphuretted products.
The elimination of the sulphur, which is effected in the form of sulphuretted hydrogen should lead to the presence of free valences which are capable of reacting and of uniting with other molecules which are substituted for the sulphur.
By way of example, the reaction may be written:
In these equations, it is the member CnH2n which is capable of uniting with other molecules, thereby converting the aliphatic, aromatic or cyclo paraflins into branched or substituted hydrocarbons.
It is known that branched hydrocarbons generally possess more marked anti-knock properties than unbranched hydrocarbons.
It is possible, moreover, that independently of the branching phenomena, the sulphuretted organic molecules produce, owing to the elimination of the sulphur, hydrocarbons which per se improve the average anti-knock properties of the motor fuel.
The treatment for carrying out the present process may be effected in the vapor phase or in the liquid phase, at atmospheric pressure or under pressure.
It is not outside the scope of the invention to apply the process with the known catalytic treatment apparatus and with the improvements made in catalytic treatment during the last few years.
Example I,--The product to be treated may be obtained for example from a crude Irak petroleum which is rich in sulphuretted organic combinations or, on the contrary, from a crude Texas petroleum to which 5 to 6% of sulphurized schist oils have beenadded.
The product, which has been completely vaporized in a' suitable still, is introduced at atmospheric pressure into a chamber filled with catalyst.
This catalyst is raised to a temperature between 350 and 450 C. but which is so regulated as to obtain the best reaction while producing the minimum quantity of gas. With a suitable adjustment, said gas can be limited to the sulphuretted hydrogen produced by the reaction and the losses are therefore reduced to a minimum. In certain cases, it is advantageous to supply to the catalysis furnace a certain quantity of steam at the same time as the motor fuel vapors. As they issue from the catalysis furnace, the vapors are condensed, the motor fuel is optionally separated from the water, then washed with soda in order to remove the dissolved sulphuretted hydrogen. A treatment with plumbite of soda, for example, is not necessary.
It has been observed that during the operation of the catalysts the same have a tendency to become covered with a more or less substantial carbon deposit which decreases th efiiciency. This deposit therefore impairs the reactions and, after some time, the catalysts have to be changed or regenerated. This regeneration may be effected by passing a current of air or steam over the worn out catalysts, care being taken to raise the temperature sufllciently to enable the reactions that destroy the carbon coating to take place.
Example II.-The motor fuel to be treated, which has previously been enriched in sulphuretted organic combinations, is heated in a closed vessel; the pressure which is set up in the vessel is obviously proportional to the temperature obtained. Th operation may be discontinuous or continuous, the product circulating in the latter case under the eflect of suitably arranged pumps. In any case, the product which has been raised to the reaction temperature is placed in the presence of similar catalysts to those referred to above.
A When it issues from the reaction chamber, the motor fuel is washed with soda in order to remove the dissolved sulphuretted hydrogen.
The products obtained by means of the treatment which is the object of the present invention contain practically no sulphur. They show considerably improved anti-knock properties and a very satisfactory susceptibility to tetraethyl lead.
While there has been described what is at present considered to be the preferred embodiments of this invention, it will be obvious to those skilled in the art that various changes and modifications may be made therein without departing from the invention, and it is, therefore, aimed in the appended claims to cover all such changes and modifications as fall within the true spirit and scope of the invention.
I claimr A process of producing motor fuels of high antlknock value by a desulfurizing and reforming action, which comprises completely vaporizing a light hydrocarbon oil containing from about 5 to 6 per cent of an added sulfurized schist oil, passing said vapors in contact with a reforming catalyst at a temperature within the range of about 300 to 500 C. and recovering a desulfurized and reformed motor fuel of .high anti-knock value.
PAUL WOOG.
US330613A 1939-05-06 1940-04-19 Treatment of hydrocarbons Expired - Lifetime US2352059A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR2352059X 1939-05-06

Publications (1)

Publication Number Publication Date
US2352059A true US2352059A (en) 1944-06-20

Family

ID=9685120

Family Applications (1)

Application Number Title Priority Date Filing Date
US330613A Expired - Lifetime US2352059A (en) 1939-05-06 1940-04-19 Treatment of hydrocarbons

Country Status (1)

Country Link
US (1) US2352059A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2530701A (en) * 1948-06-15 1950-11-21 Shell Dev Production of desulfurized gasoline
US2574451A (en) * 1949-05-09 1951-11-06 Anglo Iranian Oil Co Ltd Catalytic desulfurization of petroleum hydrocarbons
US2691623A (en) * 1950-10-17 1954-10-12 Union Oil Co Hydrocarbon conversion process
US2883437A (en) * 1958-04-10 1959-04-21 Shell Dev Alkylation process
US2883440A (en) * 1957-05-21 1959-04-21 Shell Dev Alkylation process
US2883439A (en) * 1957-05-21 1959-04-21 Shell Dev Alkylation process
US3113921A (en) * 1960-08-17 1963-12-10 Exxon Research Engineering Co Combined hydrocarbon conversion and refining process

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2530701A (en) * 1948-06-15 1950-11-21 Shell Dev Production of desulfurized gasoline
US2574451A (en) * 1949-05-09 1951-11-06 Anglo Iranian Oil Co Ltd Catalytic desulfurization of petroleum hydrocarbons
US2691623A (en) * 1950-10-17 1954-10-12 Union Oil Co Hydrocarbon conversion process
US2883440A (en) * 1957-05-21 1959-04-21 Shell Dev Alkylation process
US2883439A (en) * 1957-05-21 1959-04-21 Shell Dev Alkylation process
US2883437A (en) * 1958-04-10 1959-04-21 Shell Dev Alkylation process
US3113921A (en) * 1960-08-17 1963-12-10 Exxon Research Engineering Co Combined hydrocarbon conversion and refining process

Similar Documents

Publication Publication Date Title
JP4958792B2 (en) Selective hydrodesulfurization and mercaptan cracking processes, including interstage separation
US2073578A (en) Method of refining hydrocarbon distillates
US2001715A (en) Method of preparing organic disulphides
US2340922A (en) Desulphurization of hydrocarbon oils
US2769753A (en) Combination process for catalytic hydrodesulfurization and reforming of high sulfur hydrocarbon mixtures
NO20024718L (en) Process for step by step hydrogen treatment for naphtha desulfurization
GB935718A (en) Catalytic hydrogenative refining of hydrocarbon oils
US2352059A (en) Treatment of hydrocarbons
US2697682A (en) Catalytic desulfurization of petroleum hydrocarbons
US2143078A (en) Catalytic desulphurization of petroleum
US2901423A (en) Process for the hydrogenation of hydrocarbons
US2371298A (en) Treatment of hydrocarbon oils
US3897329A (en) Spit flow hydrodesulfurization of petroleum fraction
US1932369A (en) Removal of sulphur compounds from crude hydrocarbons
US1836183A (en) Production of mercaptans and mercaptides
US2206921A (en) Process for desulphurization of hydrocarbons
US1933508A (en) Catalytic process for destructive hydrogenation of heavy hydrocarbons and for regeneration of catalyst therefor
US2037789A (en) Treatment of hydrocarbon oils
US2522065A (en) Catalytic desulfurization and reforming process
US2198545A (en) Process for the treatment of light distillates
US2885352A (en) Process for hydrodesulfurization employing a platinum-alumina catalyst
US2657175A (en) Desulfurization of heavy petroleum oils
US1826142A (en) Process of refining hydrocarbon oils with iron salts
US2645602A (en) Sweetening hydrocarbon distillates
US2729590A (en) Desulfurization of hydrocarbon oils